CN104522163A - Apparatus and method for pasteurizing milk for feeding to calves - Google Patents

Apparatus and method for pasteurizing milk for feeding to calves Download PDF

Info

Publication number
CN104522163A
CN104522163A CN201410646171.1A CN201410646171A CN104522163A CN 104522163 A CN104522163 A CN 104522163A CN 201410646171 A CN201410646171 A CN 201410646171A CN 104522163 A CN104522163 A CN 104522163A
Authority
CN
China
Prior art keywords
milk
treatment system
controller
temperature
reactor
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201410646171.1A
Other languages
Chinese (zh)
Inventor
K.M.卡斯滕施密特
M.J.斯图赛尔
D.A.贝克
R.L.巴克
R.A.罗蒂尔
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
GEA Farm Technologies Inc
Original Assignee
GEA Farm Technologies Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by GEA Farm Technologies Inc filed Critical GEA Farm Technologies Inc
Publication of CN104522163A publication Critical patent/CN104522163A/en
Pending legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C3/00Preservation of milk or milk preparations
    • A23C3/07Preservation of milk or milk preparations by irradiation, e.g. by microwaves ; by sonic or ultrasonic waves
    • A23C3/076Preservation of milk or milk preparations by irradiation, e.g. by microwaves ; by sonic or ultrasonic waves by ultraviolet or infrared radiation
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K10/00Animal feeding-stuffs
    • A23K10/20Animal feeding-stuffs from material of animal origin
    • A23K10/26Animal feeding-stuffs from material of animal origin from waste material, e.g. feathers, bones or skin
    • A23K10/28Animal feeding-stuffs from material of animal origin from waste material, e.g. feathers, bones or skin from waste dairy products
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K50/00Feeding-stuffs specially adapted for particular animals
    • A23K50/10Feeding-stuffs specially adapted for particular animals for ruminants
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K50/00Feeding-stuffs specially adapted for particular animals
    • A23K50/60Feeding-stuffs specially adapted for particular animals for weanlings
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/003Control or safety devices for sterilisation or pasteurisation systems
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/26Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by irradiation without heating
    • A23L3/28Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs by irradiation without heating with ultraviolet light
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Animal Husbandry (AREA)
  • Zoology (AREA)
  • Nutrition Science (AREA)
  • Birds (AREA)
  • Toxicology (AREA)
  • Biomedical Technology (AREA)
  • Biotechnology (AREA)
  • Molecular Biology (AREA)
  • Physiology (AREA)
  • Dairy Products (AREA)
  • Apparatus For Disinfection Or Sterilisation (AREA)
  • Feed For Specific Animals (AREA)
  • Fodder In General (AREA)
  • Physical Water Treatments (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)

Abstract

The present invention is directed to a system and method for pasteurizing milk and colostrum for feeding to calves. The system includes a vat for storing milk or colostrum, a circulation pump and piping system, a heat exchanger for adjusting and/or maintaining milk temperature, and an ultraviolet light pasteurizing unit (''UV reactor'') that treats the milk without damaging important immunoglobulins.

Description

For to feeding the apparatus and method of to carry out pasteurize to the milk of newborn animal
The application is Chinese invention application (denomination of invention: for feeding the apparatus and method of to carry out pasteurize to the milk of newborn animal, the applying date: on March 19th, 2010; Application number: divisional application 201080018378.4).
Technical field
The present invention relates in general to fluid disinfection systems, and relates more specifically to the apparatus and method for carrying out pasteurize to the milk and colostrum of feeding newborn animal.
Background technology
The newborn animal that dairy products gather in factory feeds newborn animal with from (" the waste product ") milk that can not sell collected from the cow there that main drove is rejected because of medical science or other reason.Although feed the milk that can not sell to milk plant newborn animal seem that to milk plant operator be economical, there is such risk, namely infectious agent can directly be propagated from the mammary gland of cow by milk or effluent (shed).Other pathogen can be deposited on milk from ight soil or dirt, or the breeding in the milk that can never suitably refrigerate or store produces.
In order to reduce such risk, preferably milk or colostrum milk before feeding to newborn animal is being carried out pasteurize.Pasteurize in already known processes comprises: milk is heated to target temperature to kill objective microbe; With this temperature a period of time of maintenance.Pasteurize milk specification defines two kinds of different pasteurization methods: 1) under 145 ℉ the batch pasteurization of 30 minutes (low temperature is long-time, i.e. LTLT), or 2) under 161 ℉ between the high temperature, short time of 15 seconds pasteurize (HTST) (usually using continuous flow process).Heat and keep temperature to make bacterial concentration alive become the reduction of the order of magnitude higher than target temperature.But some thermoduric bacterias can withstand this technique.In addition, in the low-quality milk with very high bacterial concentration, some pathogens also can withstand pasteurization process.
For killing concerning the harmful bacterium of newborn animal as Escherichia coli, Bacillus cercus and salmonella, pasteurize be desirably and be required sometimes.If milk is keeping at least 30 minutes higher than 145 ℉, then these bacteriums close to 100% are successfully being killed in the pasteurize being heated to 145 ℉.A research shows, can use the lower temperature of 120 ℉, but this temperature must be maintained to few 60 minutes.
Once through pasteurize, milk can be bottled, freezing, storage, then reheat the temperature of breast-feeding to 100 ℉ ~ 110 ℉.Without the need to storage through the milk of pasteurize, because at milk through overheated pasteurize and after being cooled to supplying temperature, it is easier to utilize and can directly feeds to newborn animal.
In addition, feed in newborn animal is born two hours to colostrum and again feed in birth 12 hours to.Collecting colostrum cow soon after calving, and colostrum comprises the carbohydrate of rather high concentration, protein and antibody.Colostrum also contains immunoglobulin (Ig) (as IgG) and the growth factor of high concentration.Condensation and the loss that pasteurize can cause immunoglobulin (Ig) is carried out to colostrum.About 25% ~ 30% of the IgG concentration in first Ruzhong is damaged in the hot pasteurize of colostrum and milk.Therefore, hot pasteurize is in general favourable, but has adverse effect to milk and colostrum.Colostrum is reheating and freezing before breast-feeding, bottling and storage usually.
Ultraviolet pasteurizer also can be used for processing milk.The United States Patent (USP) 6 of the people such as Rix, 916,452 disclose: before milk being delivered to refrigerating plant and milk storage bucket in bulk, one or more UV sterilizer unit can be used while milk temperature being kept above 82.4 ℉ (28 DEG C) to carry out sterilization to milk in milk plant.Such pasteurizer is conceptually very rational, but it can not separately in milk plant's equipment because its lack for the preparation of distribute for milk and hello to the milk of newborn animal and the necessary key function of colostrum.
Need successful kill harmful bacterium but seldom or not destroy the pasteurization system of the improvement of the immunoglobulin (Ig) for optimizing newborn animal health.
Summary of the invention
The present invention relates to the system and method for carrying out pasteurize to the milk and/or colostrum of feeding newborn animal.Term used herein " milk " should be understood to comprise milk, colostrum, other newborn animal feed and any relevant additive." newborn animal " used herein comprises any milk plant animal such as milk cow, goat and sheep.
This system comprises: for storing the bucket of milk or colostrum; Circulating pump and pipe-line system; For regulating and/or keep the heat exchanger of milk temperature; And ultraviolet light pasteurize unit (" UV reactor ").Controller makes pump startup so that milk is circulated to heat exchanger, thus by milk temperature rise to 85 ℉ ~ 120 ℉, then warm milk is passed through UV reactor with kill harmful bacterium with suitable speed and frequency cycle.Then, milk can be frozen and store or directly feed to newborn animal.By milk temperature being only increased to the scope of 85 ℉ ~ 120 ℉, to the destruction much less of immunoglobulin (Ig) and milk has still carried out pasteurize safely by the UV light from UV reactor.
Be different from discontinuous pasteurizer, the temperature that UV reactor does not rely on milk carrys out kill bacteria.In fact, the independent UV light kill bacteria in 200 ~ 280 nanometer range (i.e. UVC scope (bactericidal range)).But milk temperature is important, because cold milk is stirred (churn) by pump and pipe-line system, the butter slices (butter flake) being difficult to fully be processed by UV light can be formed.By milk temperature rise to 85 ℉ or more your pupil melt to make formed butter slices or reduce its size, thus by UV reactor, milk fully to be processed.Preferably, by milk temperature rise to more than 95 ℉ and more preferably to more than 100 ℉ to guarantee the suitable milk viscosity under minimum milk oil concentration.On the other hand, milk is heated to too high temperature and can destroys useful immunoglobulin (Ig).The upper limit of the minimized temperature range of the destruction of immunoglobulin (Ig) is made to be 120 ℉, to be preferably 115 ℉ and to be more preferably 110 ℉.
The temperature range of about 85 ℉ ~ about 120 ℉ comprises the nursing temperature range of about 100 ℉ ~ about 110 ℉.If directly fed to newborn animal by milk, be then heated to the nursing temperature range of about 100 ℉ ~ 110 ℉, because the pasteurize carried out is suitable.
If milk is frozen and stores after pasteurize, then will obtain sufficient result according to the present invention in the milk temperature compared with low side of 85 ℉ ~ 120 ℉ scopes and reduce energy demand.Note, treated useless milk may need to flow to the place that newborn animal in milk plant is stayed.In this case, milk is heated above nursing temperature range and can compensates the cooling of milk when it is carried.Heat loss is with environmental condition, time between pasteurize and feeding and other factors change.Therefore, adopt the present invention, adjustable milk temperature is with these factors in any specific milk plant situation of compensation and other factors.
Can comprise according to device of the present invention: one or more UV milk pasteurizer reactor; Flow governor; Temperature controller; And for the temperature loss setting and regulate to adapt to the needs of newborn animal to the optimal milk temperature of the milk leaving this device, cause due to the time, the equipment of Distance geometry method that milk is delivered to newborn animal.
UV milk pasteurizer used in the present invention can be those UV milk pasteurizers (this patent is attached to the application by reference) of disclosed type in the United States Patent (USP) 6,916,452 of the people such as Rix.Multiple such pasteurizer can be connected and be used to reduce the number of times that milk cycles through UV reactor.
Preferably, monitoring control devices UV reactor assemblies of the present invention adjust the processing time to adapt to defective UV bulb, ballast or associated component.
Flow governor used in the present invention comprises the pump and the meter that milk are pumped across UV reactor with following speed, and described speed guarantees that the best of milk and/or colostrum is sterilized and prevents the stagnation in the pipeline relevant to UV reactor, connection and control system.Preferably, flow velocity is about 17 gallon per minute, but, according to the change of the quantity of UV reactor, size and efficiency, other flow velocity can be adopted.
Temperature controller used in the present invention can comprise sensor and heat exchanger with milk is warm or be cooled to for following optimum temperature range: for freezing and storage; For the milk from pasteurizing device is directly fed to newborn animal; Or for adapting to the temperature loss in milk pipeline, container or the miscellaneous equipment between this device and newborn animal.Pasteurizing temperature can correspondingly adjust, because in the present invention, milk temperature does not work to pasteurize.
The present invention also can comprise the vertical tube with milk volume detector, and it is for measuring the amount of milk in bucket, and calculates and the control treatment time based on milkmeter.Such as, the bucket of 100 gallons can be equipped with 100 gallons of milk or partly 5 gallons of milk is housed, the processing time that the present invention will set roughly automatically.
Device of the present invention also can comprise mobile storage bucket, and it is for being delivered to the newborn animal being positioned at remote position by the milk through pasteurize.Mobile bucket can be adiabatic and comprises for cleaning this spray ball moving bucket or device.Mobile platform also can only for carrying storage during pasteurize to have the bucket of milk.
The present invention relates to as follows:
1. milk treatment system, comprising:
There is the ultraviolet milk treating apparatus of entrance and exit;
The storage bucket be communicated with this ultraviolet milk pasteurizing device fluid;
The pump be communicated with storage bucket fluid;
Milk heat exchanger; With
The controller be communicated with heat exchanger with pump.
2. the milk treatment system of entry 1, wherein, described ultraviolet milk treating apparatus comprises:
Multiple ultraviolet milk pasteurize reactor.
3. the milk treatment system of entry 1, it comprises further:
Carry the mobile platform of described storage bucket.
4. the milk treatment system of entry 1, it comprises further:
The mobile platform of carrying milk churn; And
Described controller comprises: milk temperature regulator.
5. the milk treatment system of entry 1, wherein, described heat exchanger comprises:
Around the water leg at least partially of described ultraviolet milk treating apparatus.
6. the milk treatment system of entry 1, wherein, described ultraviolet milk treating apparatus is placed in described heat exchanger at least in part.
7. the milk treatment system of entry 1, wherein, described controller is communicated with described ultraviolet milk treating apparatus with monitoring.
8. the milk treatment system of entry 1, it comprises further:
The milk quantity sensor be communicated with described controller fluid with described storage bucket.
9. the milk treatment system of entry 1, wherein, described controller comprises the operator interface for regulating described controller.
10. the milk treatment system of entry 1, wherein, described controller comprises:
The initial timer of pasteurize.
The milk treatment system of 11. entries 1, wherein, described heat exchanger is adjusted to the milk temperature of about 85 ℉ ~ about 120 ℉ by described controller.
Further feature of the present invention and benefit will be obvious by the detailed description and the accompanying drawings of the present disclosure.
Accompanying drawing explanation
Fig. 1 is the schematic diagram according to milk treatment system of the present invention;
Fig. 2 is the perspective view according to milk treatment system of the present invention;
Fig. 3 is the perspective view of the milk treatment system of the Fig. 2 eliminating controller;
Fig. 4 is the front view of the milk treatment system of the Fig. 2 comprised according to milk storage bucket of the present invention;
Fig. 5 is according to the schematic diagram with the milk treatment system of mobile platform for carrying storage bucket of the present invention;
Fig. 6 is front view according to storage bucket of the present invention and vertical tube and phantom; With
Fig. 7 is the schematic diagram of the milk treatment system shown in Fig. 1, but has the sectional view of UV reactor.
Detailed description of the invention
In the following description of the present invention, drawing reference numeral identical in each figure will be used for representing same or analogous element.Fig. 1 ~ 5 and Fig. 7 describe according to useless milk treatment system 20 of the present invention, and it comprises: controller 22; Milk pump 24; Entry conductor 26; Delivery channel 28; Pump intake conduit 29; Ultraviolet milk treating apparatus 30 (being referred to herein as " UV reactor "); And delivery channel 32.Storage bucket 34 and mobile platform 36 (Fig. 5) are connected with milk treatment system 20 and use.
Normally, shown milk treatment system 20 uses milk pump 24 milk is pumped across entry conductor 26 and enters UV reactor 30.When milk processes in UV reactor 30, milk is heated in a heat exchanger or is cooled to and make minimize bacterial growth and do not destroy and the temperature range of the overstate immunoglobulin (Ig) wanted healthy for newborn animal.Treated milk moves to carry out temperature adjustment by delivery channel 28 and is stored in storage bucket 34.Milk storage bucket 34 can be carried on the mobile platform 36 for milk being delivered to before exceeding predetermined temperature range at treated milk newborn animal.Mobile platform 36 also can comprise the milk dispensing pump 39 for milk to be pumped to newborn animal by carrier pipe 41.
More specifically, controller 22 starts pump 24, and milk to be circulated to UV reactor 30, (warm milk preferably around having heat exchanger 38 with by milk temperature rise to 85 ℉ ~ 120 ℉, is then passed through UV reactor 30 with kill harmful bacterium with suitable speed and frequency cycle by UV reactor 30.Then, milk can be frozen and store, or directly feeds to newborn animal.By by milk temperature rise to the scope of only 85 ℉ ~ 120 ℉, to the destruction much less of immunoglobulin (Ig), and milk still carries out pasteurize safely by the UV light from UV reactor 30.
Be different from discontinuous pasteurizer, the temperature that UV reactor does not rely on milk carrys out kill bacteria.In fact, the independent UV light kill bacteria in 200 ~ 280 nanometer range (i.e. UVC scope (bactericidal range)).But milk temperature is important, because cold milk is stirred by pump and pipe-line system, the butter slices being difficult to fully be processed by UV light can be formed.By milk temperature rise to 85 ℉ or more your pupil melt to make formed butter slices or reduce its size, thus by UV reactor, milk fully to be processed.Preferably, by milk temperature rise to more than 95 ℉ and more preferably to more than 100 ℉.On the other hand, milk is heated to too high temperature and can destroys useful immunoglobulin (Ig).The upper limit of the minimized temperature range of the destruction of immunoglobulin (Ig) is made to be 120 ℉.
The temperature range of about 85 ℉ ~ about 120 ℉ comprises the nursing temperature range of about 100 ℉ ~ about 110 ℉.If directly fed to newborn animal by milk, be then heated to the nursing temperature range of about 100 ℉ ~ 110 ℉, because it is suitable for carrying out pasteurize.
If milk is frozen and stores after pasteurize, then will obtain enough results in the present invention in 85 ℉ ~ 120 ℉ scopes compared with the milk temperature of low side.Note, treated useless milk may need to be transported to the place that the newborn animal in milk plant is stayed.In this case, milk is heated above nursing temperature range and can compensates the cooling of milk when it is carried.Heat loss is with environmental condition, time between pasteurize and nursing and other factors change.Therefore, adopt the present invention, adjustable milk temperature is with these factors in any specific milk plant situation of compensation and other factors.
Preferred heat exchanger 38 used according to the invention is positioned at UV reactor 30 around.Heat exchanger 38 shown in Figure 7 and comprise entrance 62, water leg 64 and outlet 66.Water leg 64 is around UV reactor 30 and substantially coaxially to be flowed by it thus the annular space of temperature of milk regulating UV reactor 30 and carry out pasteurize just wherein to limit water, air or other heat exchanger fluid with it.Preferably, water leg 64 is made up of stainless steel, but also can use other material.Entrance 62 is communicated with the source of water or other fluid, and described fluid source can be such as hot-water heater.Preferably, hot-water heater is the special cell of heat exchanger 38, and itself and heat exchanger 38 have closed circuit and construct.
The heat exchanger of other type also can be used for the present invention, and can be arranged in any position of milk flow path.
Temperature sensor 44 is for measuring the milk temperature in whole pasteurization process.Preferably, temperature sensor 44 is the LM34 type precision Fahrenheit temperature sensor that can derive from National Semiconductor.If pasteurization process has completed and required milk temperature does not also reach, continuation has circulated until reach required temperature by milk.
In addition, controller 22 is preferably communicated with milk quantity sensor 43, described milk quantity sensor 43 preferably can derive from the integrated silicon pressure sensor (MPX5010GP of Freescale Semiconductor (www.freescale.com), Case 867b-04), it uses the long vertical tube 42 of the traps air when the liquid level of bucket 34 raises.Along with the milk horizontal plane in bucket 34 raises, the pressure in long vertical tube 42 improves.Milk quantity sensor 43 produces voltage read output signal, and this voltage read output signal is sent to controller 22, thus is that any milk in batches determines running time automatically.
Preferably, controller 22 is set by skilled erector or technician at first.Any dairy operator all can carry out at operator interface 45 other condition any of regulating to adjust in temperature, flow velocity, processing time or pasteurization process.
Controller 22 also provides display 42, and its instruction through how long and the Current Temperatures of milk, makes milk temperature can be made to get back in required scope by the recirculation of heat exchanger 38 from pasteurization process terminates.Display 42 can be dairy operator and provides any relevant information, comprises running time, flow velocity, milk temperature, component failure, maintenance requirements etc.
Finally, by after being dispensed to newborn animal or mobile platform 36 through the milk of pasteurize, milk treatment system 20 can be connected to washing system (not shown) automatically to clean and to prepare to carry out next pasteurize.
Milk treatment system 20 can comprise one or more UV milk pasteurizer reactor 30.In the illustrated embodiment, three UV reactors 30 are used.UV milk pasteurizer used in the present invention can be the United States Patent (USP) 6,916 of the people such as Rix, those UV milk pasteurizers (this United States Patent (USP) is incorporated herein by reference) of type disclosed in 452.UV reactor 30 shown in Figure 7 comprises entrance 50, outlet 60, quartz ampoule 52, UV light modulation bubble 56 (UV light modulation bubble 56 is positioned at quartz ampoule 52 inside and contacts UV light modulation bubble 56 to prevent milk).Also the pipe of other type can be used not destroyed by milk to protect UV light modulation to steep 56.Around quartz ampoule 52 are outer tubes 58 (being preferably made up of stainless steel), and outer tube 58 and quartz ampoule 52 define annular milk flow channel.Heat exchanger 38 is around outer tube 58.Milk flows through entrance 50, annular flow passage 58 (milk carries out pasteurize by UV light wherein), and flows out from outlet 60.
UV light modulation bubble 56 preferably can derive from First Light Technologies, the GIA972T5LCA/2S07/PT-18 "/4W/N/CB-061 (UV is pure) of Inc. (P.O.Box 191,212 Ideal Way, Poultney, VT 05764).Ballast used in UV reactor 30 preferably can derive from the electric ballast EVG 100 of ZED-Ziegler Electronic Devices GmbH ... 200W/230V AC.The external diameter of quartz ampoule 52 is about 1 inch, and the internal diameter of outer tube 58 is about 1.37 inches.In addition, the external diameter of outer tube 58 is about 1.50 inch diameters, and the internal diameter of water leg 64 is about 2.37 inches, but the water leg 64 of other size is also feasible.
Other combination of bulb and ballast is also feasible, and expects that this combination meets U.S.'s quality standard of electric apparatus (UL).UV reactor 30 can use to reduce the number of times that milk cycles through UV reactor by serial or parallel connection.Preferably, controller 22 of the present invention is monitored ground and is communicated with, to monitor UV reactor 30 assembly and to adjust the processing time to adapt to defective UV light modulation bubble 56, ballast or associated component.A kind of method of monitoring such assembly is the electric current that such as bulb is flow through in monitoring.If bulb does not work, then electric current is not had to flow through bulb.
Milk is pumped across UV reactor 30 with following speed by pump 24, and described speed guarantees that the best of milk and/or colostrum is sterilized and prevents the stagnation in the pipeline relevant to UV reactor 30, connection and control system.Preferably, flow velocity is about 17 gallon per minute, but, along with the size of other system component or the change of type, other flow velocity can be adopted.
Preferably, programme milk pump 24 is run with the flow velocity of about 17 gallon per minute to controller 22.When the UV reactor 30 that use one is independent, this flow velocity will produce the milk through pasteurize afterwards by UV reactor 30 about 40 " secondary ".Two UV reactors 30 of connecting are used to need by reactor 30 about 20 times, and, use three UV reactors of connecting to need by reactor 30 about 13.4 times.
For 50 gallons of useless milk, 2.9 minutes/time pass through, about 59 minutes consuming time of UV pasteurization process.This is relative to batch pasteurization heating, process and the improvement of cool time.In addition, the present invention saves time and energy-conservation, and this is mainly because without the need to being heated to so high temperature by milk.Test shows, the present invention saves the time of 30% ~ 70% relative to batch pasteurization technique.
In addition, present invention facilitates the efficiency of milk plant, because can before needs milk a few hours fill milk churn 34, and pasteurization process automatically can start with to carrying out warm, pumping, pasteurize and storage for the milk be delivered on the mobile platform 36 of newborn animal by controller 22 at reasonable time.This function is preferably by the initial timer sets of pasteurize that can manipulate on operator interface 45.
As shown in Figure 6, the present invention also can comprise the vertical tube 42 of the milk volume detector 38 with the amount for measuring milk in bucket 34.Controller 22 is calculated and the control treatment time based on the gauge of the milk in bucket 34.Such as, the bucket 34 of 100 gallons can be equipped with 100 gallons of milk or partly 5 gallons of milk is housed, the processing time that the present invention will set roughly automatically.
Device of the present invention also can comprise mobile platform 36 (Fig. 5) for the milk from pasteurizer being delivered to the newborn animal being positioned at remote position or storage bucket 34.Mobile bucket 36 can be adiabatic and comprises for cleaning this spray ball moving bucket 36 or device.Mobile platform 36 can be only for carrying support and the wheel wherein storing during pasteurize and have the bucket 34 of milk.
The present invention of comparative descriptions between the present invention and the discontinuous pasteurizer of prior art is used for the usefulness of useless milk and colostrum.
Embodiment A
In this embodiment A, for the organism of all tests, in kill harmful bacterium, standard discontinuous pasteurizer is more effective than UV pasteurizer, but, when using milk, the present invention is all effective (are 99.98% for Escherichia coli, are 100% and are 99.992% for salmonella for Bacillus cercus) for the organisms of all three kinds of tests.But when using colostrum, the present invention is really lower for the validity of the organism of all three kinds of tests, reaches the degree of the deficient validity.Need more research to improve the maximal efficiency determining the effective bactericidal action to the microorganism that first Ruzhong exists in the processing time.
In addition, for these samples, the single radial immunodiffusion of ox IgG has also been carried out.Discontinuous pasteurizer sample demonstrates the remarkable minimizing (about 43%) of IgG, and UV sample does not have the minimizing of IgG completely.Therefore, the present invention as shown in embodiment A produces more wholesome useless milk, but may not produce more wholesome colostrum.
aculture medium (milk or colostrum) before any heating.
bthe just culture medium (milk or colostrum) of (time=0) after reaching pasteurizing temperature.This about half an hour consuming time.
Embodiment B
For this embodiment, repeat to test the UV pasteurizer of milk, and increase milk and be exposed to another time of 22 minutes of UV light.These results are very similar to embodiment A, for 10 gallons of milk, have and gratifyingly kill level after the bacteriums of all three kinds of tests exposed at 15 minutes.
The Part II of research uses colostrum, and for colostrum, what embodiment A had an efficiency deficiency over the course of 15 mins for tested organism kills level.Embodiment B adopts the exposure level of 30 minutes and 45 minutes.These results show: relative to embodiment A, better for the usefulness of two kinds in described three kinds of organisms 15 minutes time.Embodiment A display has MIN usefulness for two kinds of organisms 15 minutes time but usefulness for the third organism (bacillus) cannot make us accepting.But when 30 minutes and 45 minutes expose, pasteurizer of the present invention is fully to extraordinary for the usefulness of all three kinds of organisms.
In addition, for these samples, the single radial immunodiffusion of ox IgG has also been carried out.Result shows: immunoglobulin (Ig) (IgG) does not reduce over the course of 15 mins, and immunoglobulin (Ig) (IgG) has relative minimum minimizing behind 30 minutes with 45 minutes.Therefore, relative to the discontinuous pasteurizer of prior art, the present invention reflected in Embodiment B produces more wholesome milk and colostrum.
Embodiment C
This embodiment uses colostrum, identical with Embodiment B 15,30 and 45 minutes exposure levels.These results show: UV pasteurizer of the present invention generally speaking remains effective when 30 minutes and 45 minutes, especially 45 minutes time.Uniquely possible exception may be bacillus, for bacillus, only has 45 minute exposure time to demonstrate reliable result.Result demonstrates generally kills percentage lower than test before under identical open-assembly time, but the concentration when 0 time is also higher, and this may be the reason of this reduction in killing.In the onsite application of reality, the situation that the concentration of these pathogen is unlikely tested in any position is all close to this embodiment.Therefore, such conclusion can be obtained: killing rate is all gratifying 30 minutes and 45 minutes.
In addition, for these samples, the single radial Immune proliferation also carried out about ox IgG is chemically examined.Result shows: immunoglobulin (Ig) (IgG) reduced minimum or do not reduce after 15,30 and 45 minutes.Therefore, this is the remarkable improvement relative to batch pasteurization.
acFU/ml.
Above embodiment describes the present invention and is killing three kinds of pathogen basic validity retained in all immunoglobulin (Ig)s simultaneously of milk and first Ruzhong.
There is provided the foregoing detailed description of the preferred embodiment of the invention should be readily appreciated that, and it is not intended to limit the scope of claim.In addition, term " milk " used in claim is intended to enough wide to comprise milk, useless milk, not vendible milk, colostrum or can have benefited from other newborn animal feed additive any of feeding the pasteurize before newborn animal.

Claims (11)

1. milk treatment system, comprising:
There is the ultraviolet milk treating apparatus of entrance and exit;
The storage bucket be communicated with this ultraviolet milk treating apparatus fluid;
The pump be communicated with storage bucket fluid;
Milk heat exchanger; With
The controller be communicated with heat exchanger with pump, described milk heat exchanger is adjusted to the milk temperature of 85 ℉ ~ 120 ℉ by wherein said controller.
2. the milk treatment system of claim 1, wherein said ultraviolet milk treating apparatus comprises:
Multiple ultraviolet milk treatment reactor.
3. the milk treatment system of claim 1, it comprises further:
Carry the mobile platform of described storage bucket.
4. the milk treatment system of claim 1, it comprises further:
The mobile platform of carrying milk churn; And
Described controller comprises: milk temperature regulator.
5. the milk treatment system of claim 1, wherein said heat exchanger comprises:
Around the water leg at least partially of described ultraviolet milk treating apparatus.
6. the milk treatment system of claim 1, wherein said controller is communicated with described ultraviolet milk treating apparatus with monitoring.
7. the milk treatment system of claim 1, it comprises further:
The milk quantity sensor be communicated with described controller fluid with described storage bucket.
8. the milk treatment system of claim 1, wherein said controller comprises the operator interface for regulating described controller.
9. the milk treatment system of claim 1, wherein said controller comprises:
The initial timer of pasteurize.
10. the milk treatment system of claim 1, wherein said controller is used for milk open-assembly time milk being kept in described ultraviolet milk treating apparatus 15 minutes, 30 minutes, 45 minutes or 60 minutes.。
The milk treatment system of 11. claims 1, wherein said milk temperature is 100 ℉ ~ 110 ℉.
CN201410646171.1A 2009-03-27 2010-03-19 Apparatus and method for pasteurizing milk for feeding to calves Pending CN104522163A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US12/383,830 US8127667B2 (en) 2009-03-27 2009-03-27 Apparatus for pasteurizing milk for feeding to calves
US12/383,830 2009-03-27

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
CN201080018378.4A Division CN102413710B (en) 2009-03-27 2010-03-19 Apparatus and method for pasteurizing milk for feeding to calves

Publications (1)

Publication Number Publication Date
CN104522163A true CN104522163A (en) 2015-04-22

Family

ID=42320292

Family Applications (2)

Application Number Title Priority Date Filing Date
CN201080018378.4A Expired - Fee Related CN102413710B (en) 2009-03-27 2010-03-19 Apparatus and method for pasteurizing milk for feeding to calves
CN201410646171.1A Pending CN104522163A (en) 2009-03-27 2010-03-19 Apparatus and method for pasteurizing milk for feeding to calves

Family Applications Before (1)

Application Number Title Priority Date Filing Date
CN201080018378.4A Expired - Fee Related CN102413710B (en) 2009-03-27 2010-03-19 Apparatus and method for pasteurizing milk for feeding to calves

Country Status (8)

Country Link
US (2) US8127667B2 (en)
EP (2) EP2893816A1 (en)
JP (2) JP5805620B2 (en)
CN (2) CN102413710B (en)
BR (1) BRPI1009147A2 (en)
CL (1) CL2011002346A1 (en)
RU (1) RU2584587C2 (en)
WO (1) WO2010110853A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110615151A (en) * 2019-10-28 2019-12-27 河北省微生物研究所 Pasteurization filling equipment for filling bacillus agent and application thereof

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DK200801639A (en) 2008-11-21 2010-05-22 Calvex As Improvements in or relating to the thawing of raw milk
US8127667B2 (en) * 2009-03-27 2012-03-06 Gea Farm Technologies, Inc. Apparatus for pasteurizing milk for feeding to calves
US20110318463A1 (en) * 2009-09-17 2011-12-29 Bob White Systems, Inc. System and Method for Pasteurizing Milk
US20120315364A1 (en) * 2011-06-09 2012-12-13 TOKITAE LLC, a limited liability company of the State of Delaware Heat stable vessel
CA2895362C (en) * 2012-12-18 2021-05-11 Carag Ag Apparatus and methods for pasteurization of human milk
EP3154371B1 (en) * 2014-06-10 2020-12-02 Tetra Laval Holdings & Finance SA System and method for processing liquid or semi-liquid food products
EP2957177A1 (en) * 2014-06-16 2015-12-23 Carag AG Device for pasteurization of human milk
CN104255909A (en) * 2014-10-14 2015-01-07 荣成炭谷有限公司 Sterilization method and equipment for milk
RU2600128C1 (en) * 2015-07-13 2016-10-20 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Донской государственный аграрный университет" (ФГБОУ ВПО ДГАУ) Plant for pasteurization of liquid products
KR102016436B1 (en) * 2017-08-09 2019-09-02 건국대학교 글로컬산학협력단 BREASTMILK Pasteurization SYSTEM
US10791706B2 (en) 2017-10-02 2020-10-06 Gregory John Abts Double tank milk supply system for providing a continuous supply of milk or milk products
US11134712B2 (en) 2018-08-08 2021-10-05 Mp Equipment Llc Adjustable breading machine and method of operation
CN115281246B (en) * 2022-09-15 2023-05-05 新疆豪子畜牧有限公司 Environment-friendly milk processing sterilization device and method

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3934042A (en) * 1973-07-13 1976-01-20 William Patrick De Stoutz Method and apparatus for the irradiative treatment of beverages
US4534282A (en) * 1982-05-04 1985-08-13 Marinoza Rene A Process and apparatus for treating food products
CN1091595A (en) * 1994-01-26 1994-09-07 覃祖柱 Family expenses can degrading carcinogen in it, make cholesterol become vitamin D 3Milk treatment process and device that again can sterilization
CN1379625A (en) * 1999-10-12 2002-11-13 海德罗宗控股有限公司 Sterilization of liquids using ultra-violet light
WO2008126037A1 (en) * 2007-04-16 2008-10-23 Koninklijke Philips Electronics N.V. An apparatus for producing a drink, and the use of the apparatus

Family Cites Families (54)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1730016A (en) * 1920-03-03 1929-10-01 Electropure Corp Apparatus for sterilizing liquids
US1723603A (en) * 1928-02-17 1929-08-06 Chesney Process Inc Process of sterilization and food activation
US2081243A (en) * 1933-09-08 1937-05-25 Barnett W Macy Apparatus for pasteurizing liquids
US2189279A (en) * 1937-01-25 1940-02-06 Ralph E Bitner Sterilizer
US2170402A (en) * 1937-10-01 1939-08-22 Bristol Company Automatic temperature control system
US2147912A (en) * 1938-05-02 1939-02-21 Mojonnier Bros Co Heat exchange system
US2339906A (en) * 1939-07-17 1944-01-25 Richard H Barnes Apparatus for irradiating materials
US2282024A (en) * 1940-01-24 1942-05-05 Ralph E Bitner Liquid sterilizer
US2340890A (en) 1941-02-25 1944-02-08 Lang Alphonse Method and apparatus for sterilizing, preserving, and irradiating of various liquid substances
GB639467A (en) 1946-07-10 1950-06-28 Michel Pequignot Improved apparatus for treating fluids by radiation
US2623449A (en) * 1947-01-16 1952-12-30 Losee Products Co Pasteurizer
US2550584A (en) * 1949-02-03 1951-04-24 Mittelmann Eugene Milk pasteurization method and apparatus
US2636991A (en) 1950-05-12 1953-04-28 Hanovia Chemical & Mfg Co Method and apparatus for irradiating liquids
US3092503A (en) * 1960-08-30 1963-06-04 Oscar S Gray Method and apparatus for sterilizing
FR1278161A (en) 1960-10-28 1961-12-08 Liquid sterilizer
FR1310471A (en) 1960-11-10 1962-11-30 Treatment chamber for sterilizers of water, gas or other fluids by ultra-violet rays
CH394775A (en) 1961-02-16 1965-06-30 Patrick De Stoutz William Milk processing process
FR80549E (en) 1961-07-21 1963-05-10 Device for sterilizing water by ultraviolet rays with prior sterilization of the pipes
US3182193A (en) 1962-01-03 1965-05-04 Ultra Dynamics Corp Electronically monitored liquid purification or sterilizing system
GB1212633A (en) 1968-04-03 1970-11-18 Erex Hydro Engineering Pty Ltd Improvements relating to the irradiation of fluids
US4141686A (en) 1977-03-24 1979-02-27 Lewis James H Disposable liquid sterilizer unit
RU656297C (en) 1977-06-06 1993-12-15 Всесоюзный научно-исследовательский институт электрификации сельского хоз йства Apparatus for treating milk by ultraviolet radiation
SU698591A1 (en) * 1978-07-31 1979-11-25 Всероссийский Ордена Трудового Красного Знамени Научно-Исследовательский И Проектно-Технологический Институт Механизации И Электрификации Сельского Хозяйства Milking unit
IT1123509B (en) 1979-07-31 1986-04-30 Vighi Temistocle PLANT FOR THE STERILIZATION OF LIQUIDS IN GENERAL BY ULTRAVIOLET RADIATION AND RELATED PROCEDURE
US4400270A (en) 1980-04-18 1983-08-23 Adco Aerospace, Inc. Ultraviolet apparatus for disinfection and sterilization of fluids
SU1055462A1 (en) * 1980-12-19 1983-11-23 Центральный Научно-Исследовательский И Проектно-Технологический Институт Механизации И Электрификации Животноводства Южной Зоны Ссср Installation for ultraviolet radiation of liquid
CA1159705A (en) 1982-05-14 1984-01-03 Rene A. Marinoza Apparatus for sterilizing flowable food products by electro-magnetic radiations
NL8300061A (en) * 1983-01-07 1984-08-01 Stork Amsterdam APPARATUS FOR HEAT TREATING A LIQUID PRODUCT, AND A METHOD FOR OPERATING AND CLEANING SUCH AN APPARATUS.
SU1159521A1 (en) 1983-05-30 1985-06-07 Латвийская Ордена Трудового Красного Знамени Сельскохозяйственная Академия Milk bucket
SU1217315A1 (en) 1984-01-13 1986-03-15 Латвийская Ордена Трудового Красного Знамени Сельскохозяйственная Академия Apparatus for sanitary treatment of milk
DE3414870A1 (en) 1984-04-19 1985-10-31 René 8521 Möhrendorf Stein Apparatus for drinking-water disinfection for mobile homes
GB8513170D0 (en) 1985-05-24 1985-06-26 Still & Sons Ltd W M Water purifiers
SU1303791A1 (en) * 1985-06-25 1987-04-15 Колхоз "Заря Коммунизма" Омского Р-На,Омской Обл. Automatic device for heating,transporting and dispensing milk and liquid milk products for feeding calves
US4798702A (en) 1986-09-10 1989-01-17 Tucker Robert E Sterilizer unit for fluid media and process
SE461566B (en) * 1987-06-05 1990-03-05 Alfa Laval Agri Int SET ON CONTINUOUS HEAT TREATMENT OF A VETERINARY VARIOUS FLOW VARY
DE3881473T2 (en) * 1987-10-22 1993-09-09 Duthie Jun Robert E METHOD AND STERILIZATION DEVICE.
DE9017684U1 (en) 1990-08-08 1991-11-14 Ibl Umwelt- Und Biotechnik Gmbh, 6900 Heidelberg Device for carrying out photochemical reactions
IT1247067B (en) * 1991-01-14 1994-12-12 Cartigliano Off Spa Method and equipment for the treatment of biological products.
US5571550A (en) * 1993-01-22 1996-11-05 Polny, Jr.; Thaddeus J. Methods for electroheating food employing concentric electrodes
EP0722424B1 (en) 1993-10-06 1998-08-12 Water Recovery Plc Uv apparatus for fluid treatment
FR2719483B1 (en) 1994-05-09 1996-07-05 Stoutz Jean Christian De Method and device for treating liquids by ultraviolet radiation.
RU2089061C1 (en) * 1995-06-26 1997-09-10 Республиканский научный хозрасчетный инновационный центр агропромышленного комплекса Apparatus for cooling milk and other liquid agricultural products in animal farms
US5785845A (en) 1995-11-09 1998-07-28 Colaiano; Robert Water purifying system
US5709799A (en) 1996-06-03 1998-01-20 Vortex Corporation Super ozonating water purifier
GB9611698D0 (en) * 1996-06-05 1996-08-07 Iatros Ltd Fluid processing
AUPO566097A0 (en) 1997-03-17 1997-04-10 Browne, John Phillip Fluid mixer and water oxygenator incorporating same
US6276385B1 (en) * 2000-06-09 2001-08-21 Fisher Controls International, Inc. Plug and seat positioning system for control applications
US6410071B1 (en) * 2000-07-10 2002-06-25 Louis S. Polster Method and control system for controlling pasteurization
JP2002191294A (en) * 2000-12-28 2002-07-09 Fujitec:Kk System for converting surplus milk into livestock feed
RU31188U1 (en) * 2003-03-13 2003-07-27 Полетаева Галина Павловна Preventive Sour Cream Production System
WO2005021050A1 (en) * 2003-08-22 2005-03-10 Hydro Dynamics, Inc. Method and apparatus for irradiating fluids
US7401546B2 (en) * 2003-09-09 2008-07-22 Dairy Tech, Inc. Batch pasteurizer
RU2271671C1 (en) * 2004-08-17 2006-03-20 Виктор Васильевич Марченко Method for preparing of sour milk products, method for treating of milk for effectuating the same, sour milk product preparing line and milk treating apparatus for the same line
US8127667B2 (en) * 2009-03-27 2012-03-06 Gea Farm Technologies, Inc. Apparatus for pasteurizing milk for feeding to calves

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3934042A (en) * 1973-07-13 1976-01-20 William Patrick De Stoutz Method and apparatus for the irradiative treatment of beverages
US4534282A (en) * 1982-05-04 1985-08-13 Marinoza Rene A Process and apparatus for treating food products
CN1091595A (en) * 1994-01-26 1994-09-07 覃祖柱 Family expenses can degrading carcinogen in it, make cholesterol become vitamin D 3Milk treatment process and device that again can sterilization
CN1379625A (en) * 1999-10-12 2002-11-13 海德罗宗控股有限公司 Sterilization of liquids using ultra-violet light
WO2008126037A1 (en) * 2007-04-16 2008-10-23 Koninklijke Philips Electronics N.V. An apparatus for producing a drink, and the use of the apparatus

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
郑建仙: "《功能性食品(第二卷)》", 30 September 1999, 中国轻工业出版社 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110615151A (en) * 2019-10-28 2019-12-27 河北省微生物研究所 Pasteurization filling equipment for filling bacillus agent and application thereof
CN110615151B (en) * 2019-10-28 2021-10-08 河北省微生物研究所 Pasteurization filling equipment for filling bacillus agent and application thereof

Also Published As

Publication number Publication date
US20100242744A1 (en) 2010-09-30
JP2015180217A (en) 2015-10-15
RU2011139084A (en) 2013-05-10
JP5805620B2 (en) 2015-11-04
CL2011002346A1 (en) 2012-07-06
EP2893816A1 (en) 2015-07-15
JP2012521756A (en) 2012-09-20
US8127667B2 (en) 2012-03-06
US20120210883A1 (en) 2012-08-23
BRPI1009147A2 (en) 2015-09-22
RU2584587C2 (en) 2016-05-20
US8448569B2 (en) 2013-05-28
CN102413710A (en) 2012-04-11
EP2410870A1 (en) 2012-02-01
EP2410870B1 (en) 2015-03-04
CN102413710B (en) 2014-12-17
WO2010110853A1 (en) 2010-09-30

Similar Documents

Publication Publication Date Title
CN102413710B (en) Apparatus and method for pasteurizing milk for feeding to calves
US8839713B2 (en) System for pasteurizing animal food
CN102427830B (en) UV liquid steriliser
JP2017522159A (en) Fluid sterilization system and fluid sterilization method
SE530656C2 (en) Ozone treatment of liquid foods
FI119016B (en) Apparatus for handling heat-sensitive liquid foods
CN1101500A (en) Combined super high temperature sterilizing technology
CN109924253A (en) A kind of compound continuous sterilization device of ultrasound-heat and method for disinfection for sterilization of milk
US20050112255A1 (en) Apparatus and method for microbial intervention and pasteurization of food and equipment
EP2974603B1 (en) A pasteurizer for continuously treating small volumes of liquid foods
CN208909027U (en) Steam immersion superhigh temperature system
US11910802B2 (en) Process equipment for sterilizing non transparent fluids and a method for this
CN106387045A (en) Hot water pasteurization device of fresh milk and automatic control method thereof
DK154113B (en) APPLIANCE FOR HEAT TREATMENT OF NEW MILK MILK
RU2708989C1 (en) Microwave plant for mastitis milk pasteurisation
Hariono et al. Comparative study on the physical characteristics of goat milk pasteurization through serial and circulation systems of ultraviolet method
WO2019076413A1 (en) Process equipment for sterilizing non transparent fluids and a method for this
CN210275731U (en) Ultraviolet sterilization equipment for liquid beverage
RU2106766C1 (en) Microwave unit for pasteurizing and sterilizing liquids
CN213214838U (en) Centralized liquid milk disinfection and feeding system
RU2700082C1 (en) Modular plant with infrared, ultraviolet radiation for treatment of liquid with active heat exchanger
Chambers et al. Processing quality fluid milk products
JP2010284149A (en) Simplified device for subjecting foremilk to low-temperature heating

Legal Events

Date Code Title Description
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination